Stationary diffuser

ABSTRACT

A method and apparatus for effecting washing, bleaching, or thickening, etcetera of paper pulp or the like utilizes stationary screens, yet provides efficient treatment without significant screen clogging. Pulp introduced into the bottom of a cylindrical upright vessel is caused to flow in particular radial segments and channels. Introduction of pulp into all channels of a particular radial segment, extraction of withdrawn liquid from the radial segments, removal of treated pulp from the top of the vessel, and the introduction of treating liquid between the stationary screens, are coordinated so that uniform treatment of the upwardly flowing pulp results.

This is a division of application Ser. No. 498,801 filed May 27, 1983now U.S. Pat. No. 4,441,224 which in turn is a divisional of Ser. No.374,763 filed May 4, 1982 now U.S. Pat. No. 4,468,319.

BACKGROUND AND SUMMARY OF THE INVENTION

The invention relates to a method and apparatus primarily adapted fortreating a comminuted cellulosic fibrous material with a treatmentfluid. In particular, the invention primarily relates to diffusing washwater into a cellulosic pulp mass to displace liquid already in the massto effect washing thereof.

In early stages of pulp treatment machinery development, diffusion waspracticed by providing a plurality of screens located in the bottom of atall cylindrical tank. Fresh wash water was added by a distributionsystem to the top of the pulp suspension, and the spent chemicalsolution was extracted from the tank under the screens being displacedby the fresh water diffusing downwardly by gravity through the pulpmass. Generally such diffusers were operated in series to increase thewashing efficiency. Later, stationary pulp diffusers were replaced byrotary vacuum drum filters.

In modern times, the most commercially successful diffusers haveoperated on a continuous basis. In such modern diffuser designs the pulpmass is pumped upwardly through a tank passing inbetween a series ofvertical concentric screens through which the spent liquor is extracted,wash water being introduced by generally tubular nozzles rotating in aconcentric path between pairs of concentric screens. Attempts have beenmade to build such continuous diffusers with stationary extractionscreens, however it was found that the screens had a tendency to clograpidly, resulting in channeling of the pump and resultant lowdisplacement efficiency. In order to overcome such clogging, the screenswere made movable, and in commercial installations such screens arereciprocated, moving slowly upwardly at about the speed of pulp flow agiven stroke length, and then moving rapidly downwardly (whileextraction is shut off) to clean the screens. While such diffusers workvery well and have enormous advantages over early stage technologydiffuser machinery, the necessity for reciprocating the screens resultsin undesired complications and expense. Modern day attempts to overcomesuch disadvantages, such as by providing stationary screens andintroducing gas within the screens to prevent clogging, have not metwith commercial acceptance.

According to the present invention, a method and apparatus are providedfor the continuous treatment of a fibrous suspension, such as asuspension of comminuted cellulosic fibrous material, which overcomesdrawbacks associated with conventional commercially utilized treatmentapparatus, while maintaining the advantages thereof. According to thepresent invention, stationary screens are successfully utilized toeffect uniform treatment of the fibrous material; despite the fact thatstationary screens are utilized in a continuous treatment of a fibroussuspension, no significant screen clogging - which would result innon-uniform treatment - occurs.

According to one aspect of the present invention, a method ofcontinuously treating a suspension of comminuted cellulosic fibrousmaterial is provided. While the invention is primarily directed to thediffusion washing or bleaching of paper pulp having a consistency ofabout 6 to 14%, the general principals of the invention are applicableto a variety of other treatment procedures, types of suspensions, andsuspension consistencies. For instance the invention is applicable tothe thickening of pulp.

An exemplary method of continuously treating a suspension according tothe invention utilizes a cylindrical vessel with stationary screens andmovable treatment-fluid introduction structures. The method comprisesthe following steps: (a) Defining a plurality of radial segments, and aplurality of vertical channels in each radial segment, in the vessel.(b) Introducing the suspension, adjacent the vessel bottom upwardly inthe vessel in a moving suspension column, into a cross-sectional area inthe vessel corresponding to that of approximately one of the radialsegments. (c) Introducing treatment liquid with the movable fluidintroducing structures so that shock waves acting on the stationaryscreens as a result of the fluid introduction are minimized. (d)Substantially continuously removing withdrawn fluid from the majority ofthe stationary screens' area. (e) Terminating extraction from thescreens in each radial segment approximately when the suspension isbeing introduced therein; and (f) Continuously removing from a topportion of the vessel, above the level of the screens, a portion of theentire radial extent of the suspension at the of the top of the columnpreceding the radial segment into which the suspension is beingintroduced at the bottom of the column. The further step of (g)controlling the ratio of the upward flow of suspension in each of thevertical channels so that the flow in each channel is substantially thesame as the flow in the other channels, is also preferably practiced.

In general, treatment of the suspension, according to the invention, isaccomplished by deliberately promoting channeling in a vessel includingstationary screen assemblies, and coordinating the suspensionintroduction, the suspension flow, the suspension removal, thedisplaced-liquid extraction, and the treatment liquid introduction sothat clogging will not occur, and a uniform treatment of the fiberpassing through the vessel results.

The preferred apparatus according to the present invention includes manynovel components, and a synchronization of these components to effectthe desired uniform treatment of fiber while maintaining the screensstationary. Preferably, the stationary screens are mounted on aplurality of radially extending extraction arms, the extraction armsdefining a plurality of radial segments. The screens preferably includea plurality of annular, concentric, screen assemblies, and the fluidintroducing structure comprises a generally annular nozzle assemblydisposed between each set of screens, and rotatable with respect to thescreens. The screens and nozzle assemblies define a plurality ofvertical channels. Upward movement of the suspension is controlled bythe segments and channels. While in the ensuing disclosure an exemplarypredetermined number of radial segments and vertical channels (i.e. 12radial segments and 6 vertical channels) will be disclosed, it is to beunderstood that virtually any number of segments or channels could beprovided depending upon the material being treated, the flow ratedesired, the diffusion efficiency required, etc. (e.g. 3-48 radialsegments and 2-12 vertical channels).

Suspension is introduced into the bottom of the vessel by a rotatingpulp inlet structure which has the cross-sectional shape and area ofapproximately one radial segment. The pulp inlet is connected to arotating shaft which is centrally located in the vessel, the shaft alsobeing connected to a suspension withdrawal structure, thetreatment-liquid introducing nozzle assemblies, and a structure forcontrolling the ratio of upward flow of suspension in each verticalchannel of a radial segment.

The stationary screens are constructed so that they present a minimumresistance to the upward flow of suspension, having the cross-sectionalarea of a right circular cone frustum, and having the liquid inletopenings in the screen face slanted downwardly. A plurality of screensegments can be stacked upon each other to provide multiple stages, eachstacked assembly having the cross-sectional configuration of the frustumof a right circular cone, and including interior passageways connectingeach screen of each stage to a different extraction arm. All screensegments within a given radial segment of the vessel are hydraulicallyconnected to the same, single, extraction arm.

The construction of the nozzle assembly according to the presentinvention is designed to minimize the shock waves acting upon thescreens as a result of nozzle movement. The nozzle design - whileparticularly adapted for use with the stationary-screen apparatusaccording to the invention - also is applicable to conventionalcontinuous diffusers, such as shown in U.S. Pat. No. 3,524,551. Thenozzle assembly includes a vertically extending generally linear nozzlewith fluid-introducing openings formed therein, and an annular wallstructure concentric with the vessel and annular screens, and having anincreasing crosssectional area from a point immediately following thefluid introducing structure in the direction of rotation of the nozzleto a point of connection of the annular wall structure to the nozzle.The cross-sectional area of the wall structure is such that at any pointin the rotation cycle of the nozzle assembly the volume of introducedliquid plus the nozzle volume is a constant. The nozzle may be readilyconstructed by providing a metal ring as an interior component, andplacing a polytetrafluoroethylene ring of continuously varying thicknessalong each face of the metal ring. The polytetrafluoroethylene exteriorsurfaces can be formed with circumferential ribs to maintain uniformliquid distribution to minimize resistance.

The suspension withdrawal structure located above the screens comprisesa screw conveyor assembly, or like structure, capable of removing anentire vessel radius of material at the same time. This is incontradistinction to prior art removal scrapers, such as shown in U.S.Pat. No. 3,905,766, which move each portion of suspension arcuately aswell as radially during each rotation. The screw conveyor assemblyincludes a rotating screw, which is rotatable about an axis extendingalong a radius of the vessel, the screw conveyor assembly beingrotatable with the central shaft.

Following the screw conveyor assembly in the direction of rotation ofthe shaft is a means for equalizing the flow rate within the verticalchannels of a radial segment or segments over which the conveyorassembly has passed. Such a structure preferably comprises a platemounted for rotation about a generally horizontal axis, with a forceapplied thereto a pneumatic or hydraulic cylinder or the like. Aplurality of pressure sensors located on the bottom of the plate, oneassociated with each vertical channel within a radial segment, controlthe force application provided by the cylinder. The entire assembly isrotatable with the shaft.

Extraction of displaced liquid from each of the extraction arms iscontrolled by a valve assembly so that extraction continuously takesplace from each extraction arm (and screen segments associatedtherewith) except for the approximate time period during whichsuspension is being introduced into the radial segment associated withthat extraction arm. During at least a portion of the time when theextraction is off, back-washing liquid is introduced into the extractionarm and associated screen segments in order to relieve the pulp from thescreen surfaces. A single rotary valve, rotated in synchronization withthe central shaft of the vessel, may be provided to effect extractionand back-washing.

By properly positioning the suspension introducing structure, nozzlefluid inlets, suspension withdrawal structure, and channel flow-controlstructure on the central rotating shaft, and synchronizing the rotationof that shaft with the extraction-back-wash valve, it is possible toefficiently and uniformly treat the fibrous cellulosic material passingpast the stationary screens, with minimum potential for screen clogging.

It is the primary object of the present invention to provide a simpleand effective method and apparatus (and component parts thereof) for thecontinuous treatment of a suspension with a treatment fluid. Theinvention is particularly applicable to the treatment of pulpsuspensions having a consistency of about 6-14%. This and other objectsof the invention will become clear from an inspection of the detaileddescription of the invention, and from the appended claims.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a side cross-sectional view, with portions cut away forsimplicity of illustration, of an exemplary diffusion apparatusaccording to the present invention;

FIG. 2 is a cross-sectional view of the apparatus of FIG. 1 taken alonglines 2--2 thereof;

FIG. 3 is a detail side view, partly in cross-section and partly inelevation, indicating the interconnection between the screen extractionarms, and vessel, of the apparatus of FIG. 1;

FIG. 4 is a detail cross-sectional view of a portion of the apparatus ofFIG. 3 taken along lines 4--4 thereof;

FIG. 5 is a detail cross-sectional view illustrating an exemplaryconnection between a screen ring and extraction arm in the device ofFIG. 1;

FIG. 6 is a detail cross-sectional view taken along lines 6--6 of FIG.5;

FIG. 7 is an enlarged detail crosssectional view of a portion of apreferred screen surface of the device of FIG. 1;

FIG. 8 is a top plan diagrammatic view illustrating an exemplary form ofthe interconnections between the extraction arms, an extraction controlassembly, and a back-wash liquid control assembly;

FIG. 9 is a top diagrammatic view of a means for providing extractionand back-wash, alternative to the embodiment of FIG. 8;

FIG. 10 is a cross-sectional view taken along lines 10--10 of FIG. 9illustrating a preferred valve structure utilized in the system of FIG.9;

FIG. 11 is a cross-sectional view taken along lines 11--11 of FIG. 10;

FIG. 12 is a cross-sectional view taken along lines 12--12 of FIG. 10;

FIG. 13 is a top plan view of an exemplary nozzle assembly according tothe present invention;

FIG. 14 is a side view of the nozzle assembly of FIG. 13 as viewed inthe direction of arrow Z, with portions cut away for clarity;

FIG. 15 is a top plan view of the structure of FIG. 1;

FIG. 16 is a diagrammatic showing of a linear development of keyportions of the structure of FIGS. 1 and 15, showing the synchronousoperational cooperation therebetween;

FIG. 17 is a side cross-sectional view of exemplary multi-stage screensthat may be utilized in practicing the invention; and

FIG. 18 is a diagrammatic detail crosssectional view of an exemplaryscreen stack of FIG. 17, with relative dimensions of the componentsdistorted for clarity of illustration.

DETAILED DESCRIPTION OF THE DRAWINGS

Exemplary apparatus for treating a suspension, particularly a suspensionof comminuted cellulosic fibrous material having a consistency of about6-14%, according to the present invention is shown generally byreference numeral 10 in the drawings. Major components of the apparatus10 are: A cylindrical generally upright vessel 11, having a bottomportion 12 into which the suspension to be treated is passed, and a topportion 13 from which treated suspension is withdrawn. A pulp inletstructure 14 rotatable in the bottom portion 12 of the vessel 11 forintroducing the suspension to be treated, and operatively connected to acentral rotating shaft 15, the shaft 15 disposed along the vertical axisof the vessel 11. A plurality of annular stationary screens 16,concentric with the shaft 15. A plurality of treatment-fluidintroduction structures 17, operatively connected to central shaft 15. Atreated-suspension removal structure 18 (see FIG. 15 in particular). Achannel-flow ratio equalizing structure 19 (see FIG. 15 in particular).And, a plurality of radially extending extraction arms 20, andassociated valve means 21 or 22 (see FIGS. 8 and 9 respectively), forcontrolling the extraction and supply of back-wash liquid thereto.

According to the invention, the vessel 11 is divided up into a pluralityof radial segments and a plurality of vertical channels (see segmentsA-L in FIGS. 8 and 9, and vertical channel M-R in FIG. 1), the segmentsand channels facilitating provision of a controlled channeling ofsuspension to be treated in the vessel 11. By controlling andcoordinating the extraction of liquid through screens 16, arms 20, andvalve means 21 or 22; the provision of back-wash liquid through valvemeans 21, 22; the introduction of suspension by pulp inlet 14 atpredetermined radial segments; the introduction of treatment fluid withfluid introduction structure 17; the removal of all treated suspensionalong a particular radius of vessel 11 by the removal means 18; and theequalization of flow ratio within the channels M-R by the structure 19;uniform treatment of the pulp with minimum potential for screenclogging, and without the necessity for moving the screens, ensues.

At the top portion of the vessel 13, a conventional pulp launder 25 witha pulp discharge 26 (see FIG. 15) may be provided, conventional scrapers27 in the launderer 25 moving the pulp to the discharge 26. Suitablebearing means 28 (see FIG. 1) are provided for mounting the centralshaft 15 at the top of the vessel 11 for rotation about the central axisof the vessel, and further bearing means, illustrated diagrammaticallyby reference numeral 29 in FIG. 1, may be provided adjacent the bottomportion 12 of the vessel. A suitable conventional power structure 30rotates the shaft 15 in the direction (see FIGS. 13 and 15). The shaft15 may be hollow, and treatment liquid may be introduced therein throughconduit 31, controlled by valve 32, for ultimate distribution to thefluid introduction structure 17 through hollow support arms 33 andvertical conduits 34. The manner of fluid supply may be much the same asin conventional commercial diffusion washers, such as shown in U.S. Pat.No. 3,372,087.

The pulp introduction structure 14 is illustrated most clearly in FIGS.1 and 2, and comprises a substantially pie-shaped upper portion 36,having a cross-sectional area and shape approximately the same as thatof one of the radial segments A-L. A conduit 37 extends downwardly fromthe upper portion 36, and is mounted in a polytetrafluoroethylene sleeve38 or the like for rotation with respect to the bottom portion 12 of thevessel 11. A plate 39 integral with the top portion 36 is bolted, orotherwise attached, to the central shaft 15, as illustrated in FIG. 1. Apurge liquid can be introduced between housing 12 and conduit 37 at 40(see FIG. 1).

The annular stationary screens 16 each include at least one screensurface 41 (see FIGS. 3, 5, and 7 in particular) which may be slotted,apertured, or otherwise constructed in a conventional manner, to allowliquid passage therethrough. Preferably, however, in order to minimizeresistance to suspension upward flow in the vessel 11, each screensurface 41 is provided with a plurality of downwardly slantingfluid-passage openings, as illustrated by reference numerals 42 in FIG.7. An interior supporting structure 43 preferably is provided for thescreen surfaces 41, and in order to further minimize resistance to pulpflow, it is preferred that the screen surfaces 41 are slanted withrespect to the vertical. That is, each screen surface 41 is provided sothat at its top it is closer to the interior supporting structure 43(which is essentially vertical) associated therewith than it is at thebottom (see FIGS. 1 and 3 in particular). Thus the screen structures 16spaced from the shaft 15 and the side wall of vessel 11 have thecross-sectional area of a right-circular cone frustum.

Each arcuate section of the screen structure 16 associated with each ofthe radial segments A-L is connected to the same radial extraction arm20, and only that arm 20. An exemplary manner of interconnection betweena screen structure 16 and an arm 20 is illustrated in FIGS. 5 and 6, aheader 44 being connected to the interior of its respective screenstructure 16 ay an apertured plate 45 connected to interior supportingstructure 43, and a radial extraction arm 20 being connected by a boltedflange 46 to the header 44, hydraulic connection being provided throughan orifice plate 47 or the like (see FIG. 6), with a cover plate 48 orthe like allowing access thereto. With particular reference to FIG. 8,each of the screen structures 16' in radial segment A is connectedhydraulically to the radial extraction arm 20', and physically connectedto both the extraction arm 20' and extraction arm 20".

The arms 20 can built as individual shop-fabricated units, and fieldassembled to form a complete screen and extraction arm assembly.

An exemplary manner of connection of an exemplary extraction arm 20 tothe vessel 11 to provide for withdrawal of extracted liquid, andintroduction of back-wash liquid, is illustrated in FIGS. 3 and 4. Eacharm 20 passes through an opening 49 in the side wall of the vessel 11, amachined and leveled support ring 50 being provided for supporting allof the arms 20 at their points of passage through the openings 49. Shimsmay be provided as required between the support ring 50 and the arms 20.Each arm 20 terminates in an annular housing 51 exterior of the sidewalls of vessel 11, with an arm leveling screw or the like preferablybeing provided, as indicated by reference numeral 52 in FIG. 3, betweenthe top of housing 51 and the end portion 53 of arm 20 to insureappropriate positioning of the arm 20. The bottom bearing 29 for theshaft 15 may also comprise a central locater ring for the arms 20, asillustrated in FIG. 3.

As seen most clearly in FIG. 4, the end termination 53 of eachextraction arm 20 is preferably circular in cross-section and includestwo interior conduits 54, 55, conduit 54 connected by a flexibleconnector 55 to a connection 56 which ultimately passes to an extractionheader, and conduit 55 connected through a flexible connector 57 to aconnection 58 which is connected to a back-wash liquid supply. Theposition of the arm 20 with respect to the end termination 53 also maybe appropriately adjusted by a leveling screw indicated generally byreference numeral 59 in FIG. 4.

A blank filler piece 60 (see FIG. 1) may be provided at the top of eachof the screen structures 16. Additionally, each structure 16 maycomprise a number of stages, as illustrated in FIGS. 17 and 18 whereinfour screen stages are provided associated with each structure 16. Eachentire multi-stage screen assembly 61 has the crosssectionalconfiguration of a right circular cone frustum, and a separateextraction arm is provided for connection to each stage of themulti-stage screen 61. For instance arms 20 are connected to the firststage screens 62, arms 63 are connected to the second stage 64, arms 65are connected to the third stage 66, and arms 67 are connected to thefourth stage 68. This connection is provided by interior concentricconduits 69, 70, 71, and 72 (which may be annular or tubular), asillustrated in FIG. 18.

Withdrawal of extracted liquid from the arms 20 is provided by valvemeans, to synchronize the extraction of liquid from each radial segmentof screens with respect to the position of pulp inlet 14. One manner ofproviding such valve means is illustrated in FIG. 8 wherein valve means21 are provided, comprising a solenoid operated valve 70 being connectedbetween each extraction connection 56 and an extraction header 71, and asolenoid operated valve 72 being connected between each backwash liquidconnection 58 and back-wash header 73. A central controller (not shown)controls the extraction and back-wash introduction so that for theradial segment in direct communication with the pulp inlet 14 (segment Ain diagrammatic FIG. 16) the extraction is off (e.g. about 2 seconds),and back-wash liquid is introduced into all the arcuate screen segmentsof the sceen structures 16 within that radial segment (i.e. A) for atleast part of the time that the extraction is off.

An alternative, simplified valve means 22, is illustrated in FIGS. 9through 12. In this arrangement, only one conduit 74 need be provided inoperative association with each extraction arm 20, and a central commonvalve structure 75 is provided. The common valve structure 75 includes ahollow housing 76 having a plurality of radially extending fluidconnections 77, one associated with each extraction arm 74, and a singleback-wash introduction nozzle 78 axially spaced from the connection 77.A valve 79 (normally open) controls the flow of back-wash liquid from asource 80 to the conduit 78.

A central shaft 81 is provided in housing 76, disposed along the centralaxis thereof, and has a valve member 82. The valve member 82 comprisesan upper segment 83 which has a blocking structure having an arcuateextent approximately the same as the arcuate spacing between a pair ofadjacent connections 77 (see FIG. 11), and having a bottom portion 84comprising means defining a passageway 85 which is in alignment with theblocking portion of the first valve member portion 83, and having anarcuate extent only slightly less than the arcuate extent of theblocking portion of upper valve portion 83. An extraction liquid outlet86 is in communication with the interior of housing 76 on the oppositesides thereof as the back-wash conduit 78, extracted liquid passingthrough connection 77 into housing 76 being withdrawn through theconduit 86. The rotation of shaft 81 is coincident with the rotation ofshaft 15, and in fact a mechanical connection therebetween can beprovided, as indicated by dotted line 87 in FIG. 10.

An exemplary nozzle assembly according to the present invention is bestseen in FIGS. 1, 13, and 14. Conventional nozzles in commercialcontinuous diffusers normally are merely tubes with a tapered leadingedge. Such nozzles when passing through the pulp mass create shock waveswhich are transmitted to the screens. These shock waves--it has beenfound according to the present invention--can be a substantial source ofscreen blockage. The fluid introduction structures 17 according to thepresent invention overcome these problems by greatly minimizing (oreliminating) the shock waves transmitted as a result of nozzle rotation.The structures 17 according to the present invention are preferblyutilized in the apparatus 10 according to the invention, although theyalso may be utilized in conventional commercial diffusion washers, suchas shown in U.S. Pat. No. 3,372,087.

The fluid introduction structures 17 according to the present inventionare constructed so that at any point in the rotation cycle thereof thevolume of treatment liquid plus the nozzle assembly volume issubstantially a constant. At the point in the rotation cycle where theliquid has just been added, the liquid volume is great, whereas at thepoint in the pulp mass immediately before the rotating liquidintroduction point the liquid volume is small. This can be accomplishedby construction of surface means comprising a substantially annular wallstructure 90 operatively connected to an axially extending linear liquidintroducing portion 91, the wall structure 90 having an increasingcross-sectional area from a point immediately following the liquidintroduction portion 91 to the point of conneciton of thetreatment-liquid introducing portion 91 to the wall structure 90, asillustrated most clearly in FIG. 13.

The wall structure 90 preferably is constructed by providing an annularmetal wall 92 having a constant width, and constructing a pair oftapered-width thermoplastic sheets having the same height as the metalwall 92, and having a length approximately the same as the circumference(one interior, one exterior) of the metal wall 92. A particularlysuitable thermoplastic material for the sheets ispolytetrafluoroethylene in view of its low-friction properties. Onepolytetrafluoroethylene sheet, 93 in FIG. 13, is disposed along theinterior circumference of the metal wall 92, while anotherpolytetrafluoroethylene sheet 94 is disposed along the exteriorcircumference, the sheets 93, 94 being connected to the metal annularwall 92 in any suitable manner. In order to improve flow distribution ofintroduced liquors, the exterior surfaces of the now-annular structures93, 94 can be circumferentially ribbed as illustrated by thin ribs 95 inFIG. 14. Treatment liquid is supplied to the liquid-introducing portion91 of each nozzle assembly 17 by structures 33, 34 (see FIG. 1).

At the top portion 13 of vessel 11, the treated-pulp removal structure18 is provided. This structure is seen most clearly in FIGS. 15 and 16,and comprises a structure for removing an entire radius of pulp at thetop of the vessel 11, as opposed to merely gradually moving portions ofpulp arcuately as well as radially outwardly as is done by conventionalscrapers such as shown in U.S. Pat. No. 3,905,766. One preferred formthe removing means 18 may take is a screw conveyor assembly, including ascrew 97 having a central shaft 98 disposed along a radius of the vessel11, and rotatable about that axis by any conventional powered rotatingmeans (not shown). A collecting though-blade structure 99 follows theshaft 98 in the direction of rotation (see FIG. 16 in particular). Theentire structure 18 is connected to the central shaft 15 in any suitablemanner for rotation therewith. Pulp removed by the screw 97 is depositedin launderer 25, and ultimately discharged in pulp discharge 26 bypaddles 27.

The means 19 for equalizing the upward flow rate of pulp in each channelM through R, particularly for one or more radial segments A-L, may takethe form illustrated in FIGS. 15 and 16. The means 19 in this formcomprises a plate 101 having a pie-shape, and having the dimensions ofat least one radial segment A-L (shown having dimensions ofapproximately 1 and 1/2 radial segments A-L in the embodimentillustrated in the drawings). A plurality of conventional pressuresensors 102, one associated with each vertical channel M-R, are disposedon the bottom of plate 101, and the plate is mounted for rotation withthe shaft 15, and for pivotal movement about a horizontal axis definedby shaft 103 (see FIG. 16). A force supplying means, such as a pneumaticor hydraulic cylinder 104, also mounted for rotation with the shaft 15supplies a downwardly directed force to a portion of the plate 101circumferentially spaced from the shaft 103, the force applied by thecylinder 104 being responsive to the pressure sensors 102. The structure19 thus provides sufficient back pressure on the pulp in the radialsegment into which pulp is being introduced (e.g. A in FIG. 16) toinsure that the pulp in each channel M-R is brought to a uniform level.Note that the structure 19 is not a flow controller, merely a flowequalizer, the flow rate of the pulp being determined by the flow ratethrough inlet 14 into the vessel 11.

If necessary, the entire structure 19 can be designed so that it willrise under upset conditions so that structural damage thereto will beavoided.

Exemplary structures according to the invention having been described, atypical manner of operation thereof will now be described with respectto FIG. 16, which is a linear development of a portion of the vessel 11,and clearly illustrates the synchronization of the various operativecomponents to provide the desired pulp treatment without screenclogging.

In FIG. 16, the pulp is shown being introduced through structure 14 intoradial segment A. The position of the valve member 82 of the commonvalve structure 75 is synchronized with respect to the pulp inletstructure 14 so that the upper portion 83 of the valve member 82 blocksoff the extraction flow from the extraction arm 20 associated withradial segment A, and during a portion of the time of this block-offback-wash liquid flows through connection 78, passageway 85, andconnection 77 associated with segment A to backwash all segments of thescreen structures 16 associatd with segment A. The channel flow rateequalizing structure 19 is positioned, vis-a-vis the pulp inlet 14, sothat the pressure sensors 102 are above each vertical channel M-R of theradial segment A, and thus the flow rate in the vertical channels isequalized. The treated-pulp removal means has just passed over thesegment A (and now is approximately two segments further on) and hasremoved all the pulp in the radial segment A so that furtherintroduction thereinto, under controlled conditions, is possible. Thecommon valve structure 75 has also controlled the extraction for theother radial segments so that the extraction in segment L, justpreceding segment A in the direction of rotation, just came on, and theextraction in segment B is about to come off, and back-wash liquid isabout to be introduced thereinto. Treatment liquid is introduced bystructure 91 at about radial segment L, the segment that has just beenre-filled with pulp and where the extraction has just been turned on.

It will thus be seen that according to the present invention a methodand apparatus (and component parts thereof) have been provided whicheffect the uniform, efficient treatment of suspensions utilizingstationary screens. While the invention has been primarily describedwith respect to the treatment of pulp suspensions having a consistencyof about 6-14%, a wide variety of other suspensions also may be treatedaccording to the present invention. Also, while the invention has beenprimarily described with respect to washing, by the introduction of washwater, the invention is also applicable to other processes, such asdiffusion bleaching, and thickening.

While the invention has been herein shown and described in what ispresently conceived to be the most practical and preferred embodimentthereof, it will be apparent to those of ordinary skill in the art thatmany modifications may be made thereof within the scope of theinvention, which scope is to be accorded the broadest interpretation ofthe appended claims so as to encompass all equivalent structures,methods, and devices.

What is claimed is:
 1. A fluid introducing structure comprising: arotatable substantially linear nozzle member having means defining aplurality of spaced fluid-flow providing openings therein; and asubstantially cylindrical wall having solid exterior surfaces, said wallattached to said nozzle member at a first end thereof and rotatabletherewith, and disposed adjacent said nozzle member at a second endthereof; said wall having a continuously decreasing cross-sectional areafrom said first end to said second end thereof.
 2. A structure asrecited in claim 1 wherein said cylindrical wall includes a centralmetal cylindrical member of constant cross-sectional area, and a pair ofcylindrical thermoplastic wall members, one of said thermoplastic wallmembers attached to the interior surface of said metal wall member, andthe other of said thermoplastic wall member attached to the outersurface of said metal wall member.
 3. A structure as recited in claim 2wherein said thermoplastic wall members have antifriction propertiescomparable to those of polytetrafluoroethylene.
 4. A structure asrecited in claim 2 further comprising a plurality of circumferentialribs on the exterior surfaces of said thermoplastic wall members.
 5. Astructure as recited in claim 3 further comprising a plurality ofcircumferential ribs on the exterior surfaces of said thermoplastic wallmembers.
 6. A structure as recited in claim 1 further comprising ribsformed on said wall solid exterior surfaces for improving flowdistribution of introduced liquids.
 7. A structure as recited in claim 3further comprising ribs formed on said wall thermoplastic wall membersfor improving flow distribution of introduced liquids.
 8. A structure asrecited in claim 2 further comprising ribs formed on said wallthermoplastic wall members for improving flow distribution of introducedliquids.